EP2278048A1 - Procédé de production d un dérivé de phosphine à partir d un dérivé d oxyde de phosphine - Google Patents

Procédé de production d un dérivé de phosphine à partir d un dérivé d oxyde de phosphine Download PDF

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Publication number
EP2278048A1
EP2278048A1 EP09746642A EP09746642A EP2278048A1 EP 2278048 A1 EP2278048 A1 EP 2278048A1 EP 09746642 A EP09746642 A EP 09746642A EP 09746642 A EP09746642 A EP 09746642A EP 2278048 A1 EP2278048 A1 EP 2278048A1
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Prior art keywords
aluminum
phosphine
derivative
reaction
group
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German (de)
English (en)
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EP2278048A4 (fr
Inventor
Hideo Tanaka
Manabu Kuroboshi
Tomotake YANO
Masakatsu HOSHINO
Hiromu Kawakubo
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Hokko Chemical Industry Co Ltd
Asahi Kasei Chemicals Corp
Okayama University NUC
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Hokko Chemical Industry Co Ltd
Asahi Kasei Chemicals Corp
Okayama University NUC
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Publication of EP2278048A1 publication Critical patent/EP2278048A1/fr
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    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00—Compounds containing elements of Groups 5 or 15 of the Periodic Table
    • C07F9/02—Phosphorus compounds
    • C07F9/28—Phosphorus compounds with one or more P—C bonds
    • C07F9/50—Organo-phosphines
    • C07F9/5022—Aromatic phosphines (P-C aromatic linkage)
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00—Compounds containing elements of Groups 5 or 15 of the Periodic Table
    • C07F9/02—Phosphorus compounds
    • C07F9/28—Phosphorus compounds with one or more P—C bonds
    • C07F9/50—Organo-phosphines
    • C07F9/505—Preparation; Separation; Purification; Stabilisation
    • C07F9/509—Preparation; Separation; Purification; Stabilisation by reduction of pentavalent phosphorus derivatives, e.g. -P=X with X = O, S, Se or -P-Hal2
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00—Compounds containing elements of Groups 5 or 15 of the Periodic Table
    • C07F9/02—Phosphorus compounds
    • C07F9/547—Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom
    • C07F9/655—Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom having oxygen atoms, with or without sulfur, selenium, or tellurium atoms, as the only ring hetero atoms
    • C07F9/65515—Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom having oxygen atoms, with or without sulfur, selenium, or tellurium atoms, as the only ring hetero atoms the oxygen atom being part of a five-membered ring
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B3/00—Electrolytic production of organic compounds
    • C25B3/20—Processes
    • C25B3/25—Reduction
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/582—Recycling of unreacted starting or intermediate materials

Definitions

  • the present invention relates to a method for producing a phosphine derivative represented by the following formula (2), characterized by carrying out a reduction reaction of a phosphine oxide derivative represented by the following formula (1) in a polar organic solvent using a chlorinating agent and a salt of a metal having an ionization tendency equal to or lower than that of aluminum in the presence of aluminum.
  • the present invention relates to a method for producing a phosphine derivative represented by the following formula (2), comprising subjecting a phosphine oxide derivative represented by the following formula (1) to electrolytic reduction together with a chlorinating agent.
  • Ar represents an aryl group such as a phenyl group, a phenyl group having a substituent, a heteroaromatic ring group, and a heteroaromatic ring group having a substituent
  • R represents an aliphatic hydrocarbon group or an aliphatic hydrocarbon group having a substituent
  • n represents an integer of 0 to 3.
  • the phosphine derivative according to the present invention is an important reactant widely used for an organic synthesis reaction such as Wittig reaction or Mitsunobu reaction.
  • phosphine oxide derivatives are generated as a by-product and stored in a repository or the like in large quantities as an intractable waste. If the phosphine oxide derivatives can be reduced by an appropriate method, to convert the derivatives to phosphine derivatives, it allows the regeneration and recycle of the reactant and clears up the disposal problem of the intractable waste described above once for all.
  • NON-PATENT DOCUMENT 5 As a reaction example that converts a phosphine oxide derivative to a phosphine derivative, methods where a metal hydride is allowed to act (NON-PATENT DOCUMENT 5) such as a reaction using trichlorosilane as shown by the following equation (3) (NON-PATENT DOCUMENT 1), a reaction using triethoxysilane or polymethylhydrosiloxane as shown by the following equation (4) (NON-PATENT DOCUMENT 2), a reaction using lithium aluminum hydride and cerium chloride as shown by the following equation (5) (NON-PATENT DOCUMENT 3), a reaction using lithium aluminum hydride as shown by the following equation (6) (NON-PATENT DOCUMENT 4), and a reaction using alane as shown by the following equation (7) are reported.
  • a metal hydride such as a reaction using trichlorosilane as shown by the following equation (3) (NON-PATENT DO
  • the product is a complex mixture of benzene, cyclohexadiene, cyclohexene, and the like, in addition to diphenylphosphine oxide, phenylphosphine, and diphenylphosphine, and triphenylphosphine is not produced at all.
  • triphenylphosphine oxide a method of subjecting triphenylphosphine oxide to electrolytic reduction in acetonitrile in the presence of aluminum chloride using aluminum as an anode to produce triphenylphosphine as shown by the following equation (15) (PATENT DOCUMENT 5 and NON-PATENT DOCUMENT 9), a method of treating a triphenylphosphine oxide derivative with phosphorus pentasulfide and dimethyl sulfate, and thereafter carrying out electrolytic reduction in methanol containing lithium chloride to produce triphenylphosphine as shown by the following equation (16), and a method of treating with methyl trifluoromethanesulfonate, and thereafter carrying out electrolytic reduction in methanol containing tetrabutylammonium trifluoromethanesulfonate to produce triphenylphosphine (PATENT DOCUMENT 10) are reported.
  • Aluminum used is preferably in powder form, and those previously made uniform to a proper range of particle diameter (200 to 500 ⁇ m) by a sieve are advantageously used. However, not only this adjustment costs much, but also, aluminum in powder form is easy to ignite, and thus extra care is required for handling.
  • the pentavalent phosphorus compound represented by the following formula (18) (Ar is a phenyl group, X is chlorine) to be subjected to the reaction is prepared by reacting triphenylphosphine oxide with a chlorinating agent such as phosgene, and normally, separation and purification operations are necessary after the reaction, and it is required that the chlorinating agent and a chlorination product generated as a by-product are reduced to within the limits.
  • Ar represents an aryl group such as a phenyl group, a phenyl group having a substituent, a heteroaromatic ring group, and a heteroaromatic ring group having a substituent
  • R represents an aliphatic hydrocarbon group or an aliphatic hydrocarbon group having a substituent
  • n represents an integer of 0 to 3.
  • the phosphine derivative has been successfully efficiently obtained by subjecting the phosphine oxide derivative to a reduction reaction in a polar organic solvent using a chlorinating agent, aluminum, and a salt of a metal having an ionization tendency equal to or lower than that of aluminum.
  • Ar n R 3-n P O (1) Ar n R 3-n P (2)
  • Ar represents an aryl group such as a phenyl group, a phenyl group having a substituent, a heteroaromatic ring group, and a heteroaromatic ring group having a substituent
  • R represents an aliphatic hydrocarbon group or an aliphatic hydrocarbon group having a substituent
  • n represents an integer of 0 to 3.
  • the present invention is as follows.
  • the production method of the present invention does not need to use an expensive compound and a compound having a problem in safety in a step of converting a phosphine oxide derivative to a phosphine derivative and does not also need to go through a high pressure and a high temperature. Therefore, a phosphine derivative can be industrially produced at a low cost in a safe and simple manner.
  • a phosphine dichloride derivative by reacting a chlorinating agent such as phosgene to a phosphine oxide derivative, purify and isolate the resulting phosphine dichloride derivative, and thereafter subject the product to a reduction reaction, thereby synthesizing a phosphine derivative.
  • a chlorinating agent such as phosgene
  • purify and isolate the resulting phosphine dichloride derivative purify and isolate the resulting phosphine dichloride derivative, and thereafter subject the product to a reduction reaction, thereby synthesizing a phosphine derivative.
  • the reason why the purification and isolation operations are necessary is that a chlorinating agent and a chlorination product generated as a by-product are necessary to be reduced to within the limits, and also, the conventional method has required a long time for operations and caused reduction of the yield.
  • the production method of the present invention is not affected by a chlorinating agent and a chlorination product generated as a by-product in the reduction reaction. Therefore, the reaction mixture can be directly subjected to a reduction reaction without purifying and isolating a phosphine dichloride derivative from the reaction mixture produced in a chlorination reaction, and thus the time for operation can be shortened, and the yield can be increased.
  • the conventional methods of synthesizing a phosphine derivative from a phosphine dichloride derivative have been all carried out under the reaction conditions of a high temperature of 90° to 180°C, and many methods have taken a long treatment time of several hours to 20 hours.
  • the reaction can be carried out at a lower temperature (e.g. room temperature) in a shorter time (e.g. 10 minutes or so), as compared to the conventional technology.
  • reaction intermediate product phosphine dichloride derivative
  • high-yield production is possible.
  • the first reaction is carried out using excess aluminum, and aluminum being present as a solid is separated and collected from the reaction solution by a method of filtration or the like, and the second reaction and after can be also further carried out using the collected aluminum.
  • the reaction is carried out repeatedly using the collected aluminum, whereby the second reaction and after can be carried out, and thus the reaction can be industrially advantageously carried out.
  • simple pre-treatment and electrolytic reduction are carried out, whereby a phosphine derivative can be industrially produced from a phosphine oxide derivative cheaply and safely.
  • the production method of producing a phosphine derivative represented by the following formula (2) including the step of adding aluminum and a salt of a metal having an ionization tendency equal to or lower than that of aluminum to the reaction mixture prepared by mixing a phosphine oxide derivative represented by the following formula (1) with a chlorinating agent in a polar organic solvent to carry out the reaction will be described.
  • an aryl group (Ar) of the phosphine oxide derivative represented by the following formula (1) and the phosphine derivative represented by the following formula (2) includes a phenyl group, a phenyl group having a substituent, a heteroaromatic ring group, and a heteroaromatic ring group having a substituent.
  • aryl group examples include a phenyl group, phenyl groups having a substituent that does not change under the chlorination and reduction conditions, and further, heteroaromatic ring groups such as a 2-pyridyl group, a 3-pyridyl group, a 3-thienyl group, and a 2-furyl group, and heteroaromatic ring groups having a substituent.
  • heteroaromatic ring groups such as a 2-pyridyl group, a 3-pyridyl group, a 3-thienyl group, and a 2-furyl group
  • heteroaromatic ring groups having a substituent examples include substituents such as p-methyl, p-methoxy, o-methyl, p-fluoro, p-chloro, and p-phenyl.
  • an aliphatic hydrocarbon group (R) is an aliphatic hydrocarbon group such as an alkyl group, an alkenyl group or an alkynyl group and includes those having a substituent.
  • n is an integer of 0 to 3
  • triarylphosphine oxides with n being 3 or diarylalkylphosphine oxides with n being 2 are preferably used, and specifically, triphenylphosphine oxide, tri(p-tolyl)phosphine oxide, tri(m-tolyl)phosphine oxide, tri(o-tolyl)phosphine oxide, tri(p-methoxyphenyl)phosphine oxide, tri(p-chlorophenyl)phosphine oxide, tri(2-furyl)phosphine oxide, diphenylmethylphosphine oxide, and diphenylethylphosphine oxide are preferably used, and triphenylphosphine oxide is most preferably used.
  • Ar n R
  • the chlorinating agent used in the present invention includes oxalyl chloride, phosgene, diphosgene, thionyl chloride, phosphoryl chloride, phosphorus pentachloride, perchlorobutanoyl chloride, dichlorobenzodioxol, N,N-dimethylchloromethylimmonium chloride, or N,N-diethylchloromethylimmonium chloride.
  • the chlorinating agents that generate only gas as a by-product from a chlorination reaction are preferably used, and specifically, oxalyl chloride, phosgene, diphosgene or thionyl chloride are more preferably used.
  • An equivalent molar amount or 1.01 to 1.1 mol of the chlorinating agent based on a mole of the phosphine oxide derivative is added, and the mixture is stirred at 0° to 80°C for 1 minute to 1 hour, and thereafter a reduction reaction of a next reaction step is carried out.
  • an equivalent molar amount of oxalyl chloride is added as the chlorinating agent, and the mixture is stirred at 0° to 30°C for 1 to 10 minutes and can thereafter proceed to the next reaction step.
  • the phosphine oxide derivative is used at this time in an amount of 5 to 50% by mass and preferably 15 to 35% by mass of the polar organic solvent.
  • a polar organic solvent is used as a solvent used in this reaction step and next reduction reaction.
  • the polar organic solvent refers to an organic solvent having a high permittivity. Those having a relative permittivity at 20°C of 2 or more are preferably used, and those having a relative permittivity at 20°C of 10 or more are more preferably used.
  • Specific polar organic solvent includes acetonitrile, butyronitrile, N,N-dimethylformamide, N-methylpiperidone, pyridine, chlorobenzene, chloroform, dichloromethane, propionitrile, and the like, and acetonitrile or a mixed solvent comprising acetonitrile as a main solvent is preferably used.
  • Examples of a solvent used for the mixed solvent with acetonitrile include organic solvents such as N,N-dimethylformamide, N-methylpiperidone, pyridine, tetrahydrofuran, dioxane, benzene, chlorobenzene, toluene, dichloromethane, chloroform, acetone, ethyl methyl ketone, and diethyl ether.
  • organic solvents such as N,N-dimethylformamide, N-methylpiperidone, pyridine, tetrahydrofuran, dioxane, benzene, chlorobenzene, toluene, dichloromethane, chloroform, acetone, ethyl methyl ketone, and diethyl ether.
  • the ratio of acetonitrile to an organic solvent added in the mixed solvent is normally 1:0.3 to 1:0.001, and preferably 1:0.1 to 1:0.01.
  • the reaction temperature is not particularly limited, but is preferably in the range of 0° to 100°C and more preferably 0° to 40°C.
  • Aluminum is used this time in an amount of 0.66 to 100 mol and more preferably 1 to 5 mol based on 1 mol of the phosphine oxide derivative.
  • the shape of aluminum may be any of rod-shaped, platy, foil, granular, powdery, ribbon-shaped and spherical, and shredded aluminum foil or granular aluminum that is easy for handling is preferably used.
  • examples of the metal salt of having an ionization tendency equal to or lower than that of aluminum used include chlorides, bromides, iodides, nitrates, perchlorates and sulfates of lead, tin, bismuth, aluminum, nickel, iron, cobalt, zinc, and the like, and specific examples include lead(II) bromide, lead(II) chloride, lead(II) nitrate, bismuth(III) bromide, tin(II) chloride, tin(IV) chloride, nickel(II) bromide, iron(III) chloride, iron(III) perchlorate, zinc(II) bromide, and copper(II) sulfate; the metal salt is not particularly limited as long as it is a salt of a metal having an ionization tendency equal to or lower than that of aluminum.
  • a salt of a metal having an ionization tendency equal to or lower than that of aluminum is preferably used, and a bromide or a chloride of lead, tin or bismuth is further preferably used.
  • the amount of this salt of a metal having an ionization tendency equal to or lower than that of aluminum is used in an amount of 0.0001 to 1 mol and more preferably 0.001 to 0.01 mol based on 1 mol of aluminum.
  • the period of the reduction reaction started by the addition of the salt of a metal having an ionization tendency equal to or lower than that of aluminum is not constant depending on the reaction conditions and is from 1 minute to 3 hours, and more preferably from 5 minutes to 30 minutes.
  • a phosphine derivative is obtained by separation and purification according to the conventionally known methods such as solvent extraction and recrystallization.
  • the reaction mixture contains aluminum chloride and a metal salt having an ionization tendency equal to or lower than that of aluminum, and these substances need to be removed by purification.
  • the content of aluminum chloride in the phosphine derivative after purification is preferably 10 ppm or less, and further preferably 1 ppm or less.
  • the content of the metal salt having an ionization tendency equal to or lower than that of aluminum after purification is preferably 1 ppm or less, and further preferably substantially 0 ppm.
  • the reaction in producing the phosphine derivative from the phosphine oxide derivative, it is possible to carry out the reaction using excess aluminum (first reaction), separate and collect aluminum that exists as a solid from the reaction solution by a method of filtration or the like, further produce the phosphine derivative from the phosphine oxide derivative using the collected aluminum, and repeat this process (second reaction and after). In this case, in the second reaction and after, it is not necessary to use a salt of a metal having an ionization tendency equal to or lower than that of aluminum.
  • the reaction progression without adding a salt of a metal having an ionization tendency equal to or lower than that of aluminum in the second reaction and after shows that, once aluminum is activated by a salt of a metal having an ionization tendency equal to or lower than that of aluminum, the activated state of aluminum in the system continues even repeatedly carrying out the reaction.
  • the "excess” described above refers to the use of aluminum in an amount of normally twice or more and 5,000 times or less and preferably 5 times or more and 500 times or less based on the theoretical amount of aluminum used in the reaction.
  • the theoretical amount of aluminum in the reaction is 0.67 mol based on 1 mol of the phosphine oxide derivative.
  • the reaction is repeatedly carried out using the collected aluminum, whereby the second reaction and after can be efficiently carried out and can be industrially advantageously carried out.
  • an aryl group (Ar) of the phosphine oxide derivative represented by the following formula (1) and the phosphine derivative represented by the following formula (2) includes a phenyl group, a phenyl group having a substituent, a heteroaromatic ring group, and a heteroaromatic ring group having a substituent.
  • aryl group examples include a phenyl group, phenyl groups having a substituent that does not change under the electrolytic reduction conditions, and further, heteroaromatic ring groups such as a 2-pyridyl group, a 3-pyridyl group, a 3-thienyl group, and a 2-furyl group, and heteroaromatic ring groups having a substituent.
  • heteroaromatic ring groups such as a 2-pyridyl group, a 3-pyridyl group, a 3-thienyl group, and a 2-furyl group
  • heteroaromatic ring groups having a substituent examples include p-methyl, p-methoxy, o-methyl, p-fluoro, p-chloro, and p-phenyl.
  • an aliphatic hydrocarbon group (R) is an aliphatic hydrocarbon group such as an alkyl group, an alkenyl group and an alkynyl group and includes those having a substituent.
  • n is an integer of 0 to 3
  • triarylphosphine oxides with n being 3 or diarylalkylphosphine oxides with n being 2 are preferably used, and specifically, triphenylphosphine oxide, tri(p-tolyl)phosphine oxide, tri(m-tolyl)phosphine oxide, tri(o-tolyl)phosphine oxide, tri(p-methoxyphenyl)phosphine oxide, tri(p-chlorophenyl)phosphine oxide, tri(2-furyl)phosphine oxide, diphenylmethylphosphine oxide and diphenylethylphosphine oxide are preferably used, and triphenylphosphine oxide is most preferably used.
  • the chlorinating agent used in the present invention includes oxalyl chloride, phosgene, diphosgene, thionyl chloride, phosphoryl chloride, phosphorus pentachloride, perchlorobutanoyl chloride, dichlorobenzodioxol, N,N-dimethylchloromethylimmonium chloride or N,N-diethylchloromethylimmonium chloride.
  • the chlorinating agents that generate only gas as a by-product from a chlorination reaction are preferably used, and specifically, oxalyl chloride, phosgene, diphosgene or thionyl chloride are more preferably used.
  • An equivalent molar or slightly excess amount of chlorinating agent is added to the phosphine oxide derivative, and the mixture is mixed at 0° to 80°C for 1 minute to 1 hour, and thereafter electrolysis is carried out. It is preferred that an equivalent molar amount of oxalyl chloride be added as the chlorinating agent, and the mixture is mixed at room temperature for 1 to 2 minutes, and thereafter electrolysis is carried out.
  • an electrolytic cell used for electrolytic reduction a divided cell in which an anode chamber and a cathode chamber are divided by a diaphragm is used, and as more preferable electrolytic cell, a simple undivided cell with a reactive metal as an anode is used.
  • a reactive metal a metal eluted as a metal cation by electrolysis is used.
  • a metal such as aluminum, magnesium, tin, nickel, zinc or iron or an alloy thereof is used, and aluminum is preferable.
  • a cathode is not particularly limited, and commercially available various metal electrodes and carbon electrodes can be used.
  • a polar organic solvent containing or not containing various supporting electrolytes As a solvent used for electrolytic reduction, a polar organic solvent containing or not containing various supporting electrolytes is used.
  • the polar organic solvent refers to an organic solvent having a high permittivity. Those having a relative permittivity at 20°C of 2 or more are preferably used, and those having a relative permittivity at 20°C of 10 or more are more preferably used.
  • Specific polar organic solvent includes acetonitrile, butyronitrile, N,N-dimethylformamide, N-methylpiperidone, pyridine, chlorobenzene, chloroform, dichloromethane, and propionitrile, and acetonitrile or a mixed solvent comprising acetonitrile as a main solvent is preferably used.
  • organic solvents such as N,N-dimethylformamide, N-methylpiperidone, pyridine, tetrahydrofuran, dioxane, benzene, chlorobenzene, toluene, dichloromethane, chloroform, acetone, ethyl methyl ketone and diethyl ether can be exemplified.
  • the ratio of acetonitrile to an organic solvent added in the mixed solvent is normally 1:0.3 to 1:0.001, and preferably 1:0.1 to 1:0.01.
  • a supporting electrolyte is not always necessary and can be properly added for efficient passage of electricity.
  • the supporting electrolyte is not particularly limited, and a quaternary ammonium salt such as tetra-n-butylammonium tetrafluoroborate, tetra-n-butylammonium perchlorate, tetra-n-butylammonium hexafluorophosphate, tetra-n-butylammonium bis-triflimide, tetra-n-butylammonium bromide or tetraphenylammonium bromide or a metal salt such as lithium iodide, lithium bromide, lithium tetrafluoroborate, sodium perchlorate, aluminum chloride or aluminum bromide is used.
  • a quaternary ammonium salt such as tetra-n-butylammonium tetrafluoroborate, tetra-n-butylammoni
  • Electrolytic reduction can be carried out under environmental conditions of ordinary temperature and ordinary pressure, and the reaction temperature is preferably in the range of 0° to 50°C. Electrolytic reduction can be carried out under either constant current or constant potential. From the viewpoint of ease of reaction operations or unnecessity of complex apparatus, it is preferred that electrolysis be carried out under constant current. Electrolysis can be carried out at a current density in the range of 0.1 mA/cm 2 to 1,000 mA/cm 2 and is carried out preferably in the range of 1 mA/cm 2 to 200 mA/cm 2 . The amount of electricity passed depends on the structures of the phosphine oxide derivative used and the chlorinating agent added or electrolytic reduction conditions, and electricity is passed at 1 to 10 F and preferably at 2 to 5 F per 1 mol of the phosphine oxide derivative.
  • Triphenylphosphine oxide (1.405 g, 5.0 mmol) and acetonitrile (5 mL) were weighted out into a reactor, then oxalyl chloride (0.43 mL, 5.05 mmol) was added thereto under room temperature, and the mixture was stirred for 10 minutes. Then, previously shredded aluminum foil (135 mg, 5.0 mmol) and lead bromide (18 mg, 0.05 mmol) were added to this reaction solution, and subsequently the mixture was stirred for 1 hour under room temperature to cause a reaction.
  • the reaction solution was poured into an iced 5% hydrochloric acid aqueous solution from the reactor, to terminate the reaction, and thereafter the organic layer was separated, and the water layer was extracted with ethyl acetate for 3 times.
  • the organic layers were combined into one, washed with saturated saline, dried on sodium sulfate and concentrated under reduced pressure.
  • the residue was purified with a silica gel column chromatography to give triphenylphosphine (1.189 g, 4.5 mmol, yield: 90%) and triphenylphosphine oxide (128 mg, 0.45 mmol, collection rate: 9%).
  • Triphenylphosphine oxide (1.40 g, 5.0 mmol), shredded aluminum foil (136 mg, 5.0 mmol) and acetonitrile (5 mL) were weighted out into a reactor, then oxalyl chloride (0.46 mL, 5.1 mmol) was added thereto under room temperature, and the mixture was stirred at the same temperature for 10 minutes. Subsequently, lead bromide (18 mg, 0.05 mmol) was added to this reaction solution, and the mixture was stirred for 30 minutes at room temperature. Thereafter, the reaction solution was poured into an iced 5% hydrochloric acid aqueous solution from the reactor, to terminate the reaction.
  • Triphenylphosphine oxide (1.405 g, 5.0 mmol) and acetonitrile (5 mL) were weighted out into a reactor, then oxalyl chloride (0.43 mL, 5.05 mmol) was added thereto under room temperature, and the mixture was stirred for 10 minutes. Then, previously shredded aluminum foil (135 mg, 5.0 mmol) was added to this reaction solution, and subsequently the mixture was stirred for 1 hour under room temperature to cause a reaction. The reaction solution was poured into an iced 5% hydrochloric acid aqueous solution from the reactor, to terminate the reaction, and thereafter the organic layer was separated, and the water layer was extracted with ethyl acetate for 3 times.
  • the reaction solution was taken out with a syringe and poured into an iced 5% hydrochloric acid aqueous solution, and further, the granular aluminum was washed with ethyl acetate, and a wash liquid was also poured into the iced 5% hydrochloric acid aqueous solution as well.
  • the organic layer was separated, and the water layer was extracted with ethyl acetate for 3 times. The organic layers were combined into one, washed with saturated saline, dried on sodium sulfate and concentrated under reduced pressure.
  • triphenylphosphine (1.26 g, 4.82 mmol, yield: 96%) and triphenylphosphine oxide (28 mg, 0.10 mmol, collection rate: 2%) (first reaction).
  • Triphenylphosphine oxide (1.401 g, 5.0 mmol) and acetonitrile (5 mL) were weighted out into a reactor containing the granular aluminum collected after the first reaction, then oxalyl chloride (0.46 mL, 5.10 mmol) was added thereto under room temperature, and the mixture was stirred for 1 hour to cause a reaction.
  • the reaction solution was taken out with a syringe and poured into an iced 5% hydrochloric acid aqueous solution, and further, the granular aluminum was washed with ethyl acetate, and a wash liquid was also poured into the iced 5% hydrochloric acid aqueous solution as well.
  • the organic layer was separated, and the water layer was extracted with ethyl acetate for 3 times. The organic layers were combined into one, washed with saturated saline, dried on sodium sulfate and concentrated under reduced pressure.
  • triphenylphosphine (1.23 g, 4.67 mmol, yield: 93%) and triphenylphosphine oxide (40 mg, 0.14 mmol, collection rate: 3%) (second reaction).
  • Triphenylphosphine oxide (1.40 g, 5.0 mmol) and acetonitrile (5 mL) were weighted out into a reactor containing the granular aluminum collected after the second reaction, then oxalyl chloride (0.46 mL, 5.10 mmol) was added thereto under room temperature, and the mixture was stirred for 1 hour to cause a reaction.
  • the reaction solution was taken out with a syringe and poured into an iced 5% hydrochloric acid aqueous solution, and further, the aluminum granules were washed with ethyl acetate, and a wash liquid was also poured into the iced 5% hydrochloric acid aqueous solution as well.
  • the organic layer was separated, and the water layer was extracted with ethyl acetate for 3 times. The organic layers were combined into one, washed with saturated saline, dried on sodium sulfate and concentrated under reduced pressure.
  • triphenylphosphine (1.22 g, 4.63 mmol, yield: 92%) and triphenylphosphine oxide (10 mg, 0.04 mmol, collection rate: 0.7%) (third reaction).
  • triphenylphosphine oxide An electricity of 3F/mol was applied to triphenylphosphine oxide (8 hours), and thereafter, the mixed solution after the reaction was added to an iced 5% hydrochloric acid aqueous solution, and the mixture was shaken up well and extracted with ethyl acetate. The extracts were combined into one, washed with saturated saline, dried on sodium sulfate and then concentrated under reduced pressure. As a result of analyzing a residue with a gas chromatography, it was revealed that triphenylphosphine was produced at a yield of 85% and 6% of triphenylphosphine oxide was collected.
  • Electrolytic reductions were carried out in the same manner as in Example 35 except for passing the amounts of electricity shown in Table 7.
  • Table 7 Study of Amounts of Electricity Passed Amount of Electricity Passed (F/mol) Yield (%) a Triphenylphosphine Raw Material Collection Example 47 2 72 15 Example 48 4 82 7 a Yields were measured by detection by gas chromatography. 1,4-diisopropylbenzene was used as an internal standard substance.
  • Electrolytic reductions were carried out in the same manner as in Example 35 except for using phosphine oxide shown in Table 8 in place of triphenylphosphine oxide.
  • Table 8 Study of Aryl Groups such as Phenyl Group and Heteroaromatic Ring Group Having Substituent Phosphine Oxide Yield (%) a Phosphine Derivative Raw Material Collection
  • Example 50 Trimesitylphosphine Oxide 73 17
  • Example 51 Trifurylphosphine Oxide 70 23 a Yields were measured by detection by gas chromatography. 1,4-diisopropylbenzene was used as an internal standard substance.
  • the technology of the present invention can be suitably used in the fields of pharmaceutical and chemical industries and the like.

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EP09746642A 2008-05-15 2009-05-14 Procédé de production d un dérivé de phosphine à partir d un dérivé d oxyde de phosphine Withdrawn EP2278048A4 (fr)

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CN103044288A (zh) * 2012-12-06 2013-04-17 浙江工业大学 从Mitsunobu反应废渣中再生偶氮二甲酸二异丙酯和三苯基膦的方法
CN103342719A (zh) * 2013-07-17 2013-10-09 四川大学 一种非金属还原三级膦氧化物制备三级膦的方法
CN109136972A (zh) * 2017-06-28 2019-01-04 中国科学技术大学 一种取代的磷酰胺类化合物的制备方法

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JP5665003B2 (ja) * 2010-04-16 2015-02-04 国立大学法人 岡山大学 ホスフィンオキシド誘導体からのホスフィン誘導体の直接製造法
US9246187B2 (en) * 2013-03-14 2016-01-26 Uchicago Argonne, Llc Non-aqueous electrolyte for lithium-ion battery
CN115323406B (zh) * 2022-08-15 2024-09-17 无锡绿能电合科技有限公司 一种磷酸三酯类化合物的电化学制备方法

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CN103044288A (zh) * 2012-12-06 2013-04-17 浙江工业大学 从Mitsunobu反应废渣中再生偶氮二甲酸二异丙酯和三苯基膦的方法
CN103342719A (zh) * 2013-07-17 2013-10-09 四川大学 一种非金属还原三级膦氧化物制备三级膦的方法
CN103342719B (zh) * 2013-07-17 2015-11-11 四川大学 一种非金属还原三级膦氧化物制备三级膦的方法
CN109136972A (zh) * 2017-06-28 2019-01-04 中国科学技术大学 一种取代的磷酰胺类化合物的制备方法

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WO2009139436A1 (fr) 2009-11-19
US20110065961A1 (en) 2011-03-17

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